IP Library Granted Patent US 10,562,874
Granted Patent B2
US 10,562,874 · App. 16/346,361 · Granted Feb 18, 2020

Process for the recovery of furfural

Inventors: Juben Nemchand Chheda (Houston, TX); Charu Ehrenreich-Gureja (Amsterdam, NL); Jean Paul Andre Marie Joseph Ghislain Lange (Amsterdam, NL)
Assignee: SHELL OIL COMPANY
C07D307/48B01D3/143B01D3/36C07D307/50
View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 10,562,874
App. No.
16/346,361
Granted
Feb 18, 2020
Kind
B2
Abstract

A process for the extraction of furfural from a composition comprising furfural, water, at least one organic acid and an oxygenate solvent with a boiling point higher than that of furfural. The process includes: (a) subjecting the composition to a first liquid-liquid separation step to provide: (i) an organic phase; (b) subjecting the organic phase of step (a) to a first distillation step to provide: (i) a first top stream; (c) subjecting the first top stream of step (b) to a second liquid-liquid separation step to provide: (i) a second top stream; and (d) subjecting the second top stream of step (c) to a second distillation step to provide: (i) a third top stream comprising a furfural-water azeotrope, and (ii) a third bottom stream comprising furfural.

Claims (22)

1. A process for the extraction of furfural from a composition comprising furfural, water, at least one organic acid and an oxygenate solvent with a boiling point higher than that of furfural, said process comprising:

(a) subjecting the composition to a first liquid-liquid separation step to provide:

an organic phase comprising the oxygenate solvent, furfural, and a portion of the at least one organic acid; and

an aqueous phase comprising the remainder of the at least one organic acid;

(b) subjecting the organic phase of step (a) to a first distillation step to provide:

a first top stream comprising furfural, and a portion of at least one organic acid; and

a first bottom stream comprising the oxygenate solvent;

(c) subjecting the first top stream of step (b) to a second liquid-liquid separation step to provide:

a second top stream comprising a portion of the furfural and a portion of at least one organic acid; and

a second bottom stream comprising a portion of the furfural and a portion of the at least one organic acid;

(d) subjecting the second top stream of step (c) to a second distillation step to provide:

a third top stream comprising a furfural-water azeotrope; and

a third bottom stream comprising furfural; and

(e) subjecting the second bottom stream to a third distillation step to provide:

a fourth top stream comprising a portion of the furfural which is recycled back to feed the second liquid-liquid separation step, and

a fourth bottom stream comprising water and the at least one organic acid.

2. The process according to claim 1 , wherein the composition is derived from a product stream of a pentose dehydration step wherein a pentose feed stream is dehydrated.

3. The process according to claim 2 , wherein the pentose feed stream is derived from the hydrolysis of a lignocellulosic biomass.

4. The process according to claim 1 , wherein the oxygenate solvent is selected from the group consisting of: propyl guaiacol; propyl syringol; guaiacyl propanol, syringyl propanol; nonyl phenol; o-, m-, p-substituted cresols; guaiacol; 2-methoxy-4-propylphenol; eugenol; 2,6-xylenol; sec-butyl phenol; 2,5-xylenol; and any combination thereof.

5. The process according to claim 1 , wherein a portion of the first bottom stream of step (b) comprising the oxygenate solvent is recycled into the first liquid-liquid separation step.

6. The process according to claim 1 , wherein a portion of the third top stream from step (d) comprising the furfural-water azeotrope is recycled back to feed either the first distillation step or the first liquid-liquid separator.

7. The process according to claim 1 , wherein the second bottom stream of step (c) comprising a portion of the furfural and a portion of the at least one organic acid is recycled back to feed the first liquid-liquid separator.

Assignments (2)
CHANGE OF NAME Recorded Mar 7, 2022
From: SHELL OIL COMPANY
To: SHELL USA, INC.
Reel/Frame 059694/0819 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 29, 2021
From: CHHEDA, JUBEN NEMCHAND; EHRENREICH-GUREJA, CHARU; GHISLAIN LANGE, JEAN-PAUL ANDRE MARIE JOSEPH
To: SHELL OIL COMPANY
Reel/Frame 058228/0796 →